Method for production of nitrate-containing products from undercooling melts

ABSTRACT

The invention concerns a method for the production of nitrate containing products (fertilizers, technical products) from undercooling melts, wherein a XN—water solution is evaporated up to a content of 50-99.8 weight % XN, where X is one or more selected from Ca, Mg, NH, Na and K, and N means nitrate. The preferred range of XN is 70-99.5 weight %. The melt is cooled down to and kept at a temperature at or below the crystallisation point and finely divided solid XN powder consisting of the equilibrium phases is added to the melt. Melt drops are then formed and allowed to cool and solidify during up to 70 seconds. It is preferred to use a cooling belt for solidification of the particles. The belt is cooled by air, water, oil or another medium.

The invention concerns production of nitrate-containing products(fertilizers, technical products) from undercooling melts.

Pure CN (Ca(NO₃)₂) melts at 560° C. and this very high temperature isinconvenient for particulation. In order to use devices like centrifugalor nozzle prilling equipment or pan/drum granulators, the CN melt has tohave compositions that contain 5-8 weight % ammonium nitrate (AN).Today, all prilled or granulated CN contains this amount of AN inaddition to 14-16 weight % water (crystal water). If the ammoniumnitrate content is removed from the melt, the composition undercooles tosuch an extent that prilling/granulation is not possible.

There is still a need for CN without AN and it is desirable to findmethods to produce CN-water solid easily, in large quantities.

From British Patent No. 392 531 it is known a process for production ofdistributable and non-caking fertilizers containing calcium nitrate.According to this patent, a calcium nitrate/water solution is evaporatedto a sandy-pasty consistency in which it contains about 90-95 weight %calcium nitrate (calculated as anhydrous calcium nitrate). Thereafterthe concentrated product is converted without any substantial furtherconcentration, into granular form by mechanical disaggregation in bulkat a temperature of 50-100° C. This method gives salt deposits onequipment and a flaked, dusty product. The method is thereforeconsidered not well suited for large-scale production of CN.

From a CN-water solution CN*4H₂O crystals can be obtained incrystallization processes well described in the literature. Suchcrystals are available in the markets. Such crystals contain 69-70weight % CN, but normally they have a high caking tendency and over timethey become hard and difficult to handle. Thus, it is not desirable tomake a crystalline material.

By mapping the phase diagram (from Gmelin) of the system CN-AN-Water, ithas been possible to find a rather narrow melt composition region thatcan be particulated with ordinary plant equipment and today granulatedor prilled CN contains 77-80 weight % CN, 5-8 weight % AN and 15-17weight % water.

By studying the phase diagram of CN-water (FIG. 1) it can be seen thatthe following solid compounds can be formed in the system:

-   Ca(NO₃)*4H₂O-   Ca(NO₃)*3H₂O-   Ca(NO₃)*2H₂O-   Ca(NO₃)₂

Further, it can be realized that according to the CN-water system, allCN concentrations above 70 weight % should solidify, meaning that allliquid should have disappeared at equilibrium if temperature is below40-43° C. Further, it can be seen that by cooling a CN-water solutionwith CN less than 70 weight %, CN*4H₂O crystals will be formed.

The object of the invention is to obtain a method to produce highquality solid CN-water particles easily, in large quantities. Anotherobject is to obtain a production method that could be applied generallyfor nitrate containing salts that very often tend to form super coolingmelts.

These and other objects of the invention are obtained with the method asdescribed below, and the invention is further defined and characterisedby the accompanying patent claims.

The invention thus concerns a method for the production of nitratecontaining products (fertilizers, technical products) from undercoolingmelts, wherein a XN-water solution is evaporated up to a content of50-99.8 weight % XN, where X is one or more selected from Ca, Mg, NH₄,Na and K, and N means nitrate. The preferred range of XN is 70-99.5weight %. The melt is cooled down to and kept at a temperature at orbelow the crystallisation point and finely divided solid XN powderconsisting of the equilibrium phases is added to the melt. Melt dropsare then formed and allowed to cool and solidify during up to 70seconds, preferably 20-70 seconds. It is preferred to use a cooling beltfor solidification of the particles. The belt is cooled by air, water,oil or another medium.

The melt temperature is preferably kept 0-10° C. below thecrystallization point of the melt. When calcium nitrate particles areproduced, CN*2H₂O and CN*3H₂O are used as seed particles. The particlesformed have a particle size between 0.2 and 0.8 mm, preferably between0.4 and 0.6 mm. Particles could be made from a melt consisting of 74weight % calcium nitrate, 14 weight % potassium nitrate and 12 weight %water. Solid particles can also be produced consisting of a homogenousmixture of nitrates, chlorides and crystal water. An example of this isparticles made from a melt consisting essentially of 50 weight % calciumnitrate, 4 weight % ammonium nitrate, 26.5 weight % calcium chloride and18-20 weight % water.

Several experiments were carried out in order to try to make particlesof the melts.

EXAMPLE 1 Granules (For Comparison)

CN-water solutions were evaporated to above 70, 75 and 78 weight % CN.

The various melts were sprayed onto a rotating laboratory pan granulatorcontaining solid NH—CN (calcium nitrate from Norsk Hydro ASA) in variousratios and at various temperatures.

None of the trials succeeded as the liquid/melt did not solidify. Thewhole matrix (solid CN+melt) turned into a sticky slurry that could notbe processed with liquid/solid ratios within acceptable limits.

EXAMPLE 2 Prills (For Comparison)

Melts with the CN concentrations mentioned above, were kept attemperatures close to the crystallization point given by the literature.Finely crushed NH—CN were mixed into the melt subsequent to pumping themelt at high pressure to nozzles where drops were formed and allowed tocool down to 20° C. for 5-10 seconds.

As cooling medium oil and air were tried. Solid particles did not formdue to under-cooling.

EXAMPLE 3 Making Pastilles

Trial 1 (For Comparison):

Droplets of CN-melts with CN concentrations above 70, 75 and 78 weight %pure CN where allowed to cool on a chilled metal plate down to 10° C.for several minutes. The melt-drops turned into viscous, sticky liquid,solid particles did not form.

Trial 2 (For Comparison):

Same procedure as above but now finely divided solid CN powder was addedto the melt before setting the droplets on the plate. Solids of NH—CNand crushed CN*4H₂O crystals were applied.

The melt-droplets turned into slurries with no particle strength as theycooled down.

Trial 3 (According to the Invention):

CN melt having 23 weight % water and 77 weight % CN were allowed to coolon a plate for 48 hours at 20° C. A white solid material was formedduring this time

Now clearly the melt had turned into a strong solid material over thesehours and X-ray analysis showed that the material consisted of CN*2H₂Oand CN 3*H₂O.

However, the solidifying time was too long for a convenientparticulation process.

Trial 4a (According to the Invention):

Same procedure as in trial 1, but now a CN-melt consisting of 23 weight% water and 77 weight % CN was cooled down to 50-55° C. and 2 weight %crushed material from trial 3 was thoroughly mixed into the melt.

As the drops cooled, crystals were formed and during-30-70 second hardpastilles were formed with particle strength above 1 kg. As time passed,particle strength became substantially higher.

Particles did form with this procedure and the crucial part of thisprocedure was obviously to add finely divided solid material consistingof the equilibrium phases of the system at room temperature. (CN*2H₂Oand CN*3H₂O)

Trial 4b (According to the Invention):

Same procedure as trial 4a but now melt composition was 25 weight %/75weight % and 21.5 weight %/78.5 weight % (H₂O/CaN).

Trial 5 (According to the Invention):

Same procedure as in Trial 4, after reducing the temperature of the melt(23% weight % H₂O/77% weight % CN) to approximately 45° C. the finelydivided solid material was mixed in as seeding particles. As crystalsstarted to form in the beaker, drops were allowed to fall on the coolingplate and simultaneously pure melt (23 weight %/77 weight %) withtemperature below 50° C. was added to the beaker, while stirring.

In this way drops containing solid crystals with the right compositionwere continuously formed and solidified on the metal plate just byadding one portion of solid material to make the crystallization start.

However, 40-70 seconds are too long time for using a granulation orprilling technique with an acceptable recycling ratio.

To use procedure 5 for producing large quantities of particles, a way ofobtaining 40-70 second crystallization time was looked for.

EXAMPLE 4 Making CN Pastilles in Industrial Scale (According to theInvention)

Experiments were carried out on a moving steel cooling belt (asdescribed in U.S. Pat. No. 5,326,541) that is kept at a low temperatureby using water as cooling agent. On this belt a rotating drum withnozzles, supply drops that can solidify on the belt. A plant test wascarried out with CN melt (23 weight %/77 weight %).

By using procedure described in “Trial 5”, several hundred kg of CNparticles (pastilles) were produced on the cooling belt.

EXAMPLE 5 Making MgN Pastilles (According to the Invention)

Trial 5 in Example 3 was repeated by replacing CN melt with 1: MgN-watermelt having composition 67 weight % MgN and 33 weight % H₂O (boilingpoint 180° C.) and 2: MgN-water melt with composition 58 weight % MgNand 42 weight % (boiling point 155° C.). Both melt 1 and 2 were cooleddown to 30° C. by procedure mentioned in trial 5 (Example 3). Lettingcomposition 1 and 2 solidify in an exsiccator for 3 days, and then crushthe solids formed into a fine powder made seeding material.

With melt 1 and 2 and the procedure described we obtained MgN*4H₂O andMgN*6H₂O respectively. MgN*6H₂O was made also without seeding materialas the MgN*6H₂O melt very easily solidified.

EXAMPLE 6 Making Pastilles of MGN-AN and CN (According to the Invention)

A melt consisting of 67 weight % CN, 4.0 weight % AN, 10 weight % MgNand 20 weight % water was held at 110° C. The melt was cooled down to65° C. and seeding material thoroughly mixed in as drops were allowed tofall on a cold metal plate.

During 60 seconds on the plate hard pastilles were formed. Letting themelt composition crystallize in an exsiccator for 2-3 days and thengrinding to a fine powder made seeding material.

EXAMPLE 7 Mixture of CN, AN and CaCl₂ (According to the Invention)

A melt consisting of 50 weight % CN, 4 weight % AN, 26.5 weight % CaCl₂and 18-20 weight % water was made by melting a mixture of NH—CN andCaCl₂*2H₂O (130-140-C).

By using procedure described in 4 b (seeding material added at 120° C.)nice particles were formed within 30 seconds on a cold steel plate. Theparticles consisted of homogenously solidified CaN-AN CaCl₂ particles.

EXAMPLE 8 Mixture of CN and KN (According to the Invention)

A melt consisting of 74 weight % CN, 14 weight % KN and 12 weight %water was made, by evaporating water from a CN—KN—H₂O solution. The melttemperature was reduced to 86° C., app. 5-6° C. above crystallizationpoint. 3 weight % finely grained seed material was thoroughly mixed inand droplets allowed falling on to a cold metal plate (23° C.).

During 50-60 seconds hard pastilles/particles formed on the plate.

The right seeding material was made by letting the melt compositioncrystallise in an exsiccator over 2-3 days and then grind to powder thesolid formed.

Thus, by applying:

-   -   correct melt or CN-water composition    -   correct temperature of the melt (at or below cryst. point)    -   correct seeding material (consits of equilibrium phases of the        solidifying material)    -   a cooling belt or a similar system that allows 20-70 seconds or        more for crystallization,

it has been possible to find a procedure for producing solid CNparticles (CN+crystal water) without AN. The procedure can be appliedfor making solids of several nitrate systems containing Ca, Mg, K, Na,NH₄ or mixtures of these nitrates or mixtures of nitrates and chlorides.

1. Method for the production of nitrate containing products(fertilizers, technical products) from undercooling melts, wherein aXN—water solution is evaporated up to a content of 50-99.8 weight % XN,where X is one or more selected from Ca, Mg, NH₄, Na and K, N isnitrate, the melt is cooled down to and kept at a temperature at orbelow the crystallisation point, finely divided solid XN powderconsisting of the equilibrium phases is added to the melt, where aftermelt drops are formed and allowed to cool and solidify during up to 70seconds.
 2. Method according to claim 1, wherein the content of XN is70-99.5 weight %.
 3. Method according to claim 1, wherein a cooling beltis used for solidification of the particles.
 4. Method according toclaim 3, wherein the belt is cooled by air, water oil or another medium.5. Method according to claim 1, wherein the melt drops are cooled andsolidified during 20-70 seconds.
 6. Method according to claim 1, whereinthe temperature is kept preferably 0-10° C. below startingcrystallization point of the melt.
 7. Method according to claim 1,wherein calcium nitrate is produced and CN*2H₂O and CN*3H₂O are used asseed particles.
 8. Method according to claim 1, wherein particles areformed with particle size between 0.2 and 0.8 mm, preferably between 0.4and 0.6 mm.
 9. Method according to claim 1, wherein particles are madefrom a melt consisting of 74 weight % calcium nitrate, 14 weight %potassium nitrate and 12 weight % water.
 10. Method according to claim1, wherein solid particles consisting of a homogenous chemical mixtureof nitrates, chlorides and crystal water were produced.
 11. Methodaccording to claim 10, wherein solid particles are made from a meltconsisting essentially of 50 weight % calcium nitrate, 4 weight %ammonium nitrate, 26.5 weight % calcium chloride and 18-20 weight %water.